“Ion-imprinting” strategy towards metal sulfide scavenger enables the highly selective capture of radiocesium

Highly selective capture of radiocesium is an urgent need for environmental radioactive contamination remediation and spent fuel disposal. Herein, a strategy is proposed for construction of “inorganic ion-imprinted adsorbents” with ion recognition-separation capabilities, and a metal sulfide Cs2.33Ga2.33Sn1.67S8·H2O (FJSM-CGTS) with “imprinting effect” on Cs+ is prepared. We show that the K+ activation product of FJSM-CGTS, Cs0.51K1.82Ga2.33Sn1.67S8·H2O (FJMS-KCGTS), can reach adsorption equilibrium for Cs+ within 5 min, with a maximum adsorption capacity of 246.65 mg·g−1. FJMS-KCGTS overcomes the hindrance of Cs+ adsorption by competing ions and realizes highly selective capture of Cs+ in complex environments. It shows successful cleanup for actual 137Cs-liquid-wastes generated during industrial production with removal rates of over 99%. Ion-exchange column filled with FJMS-KCGTS can efficiently treat 540 mL Cs+-containing solutions (31.995 mg·L−1) and generates only 0.12 mL of solid waste, which enables waste solution volume reduction. Single-crystal structural analysis and density functional theory calculations are used to visualize the “ion-imprinting” process and confirm that the “imprinting effect” originates from the spatially confined effect of the framework. This work clearly reveals radiocesium capture mechanism and structure-function relationships that could inspire the development of efficient inorganic adsorbents for selective recognition and separation of key radionuclides.

Cs (t 1/2 ~30.17 years) is one of the major sources of γ radioactivity in spent fuel 1 . 137Cs + ions are highly soluble and migrate easily in the environment, and thus can be hazardous to human health and entire ecosystem 2,3 .For example, large quantities of 137 Cs + ions have been released into the environment during the Fukushima nuclear accident, which has resulted in total radioactivity levels in a variety of organisms above the limit value (100 Bq kg −1 ) after many years [4][5][6] . 137Cs + waste liquids can be generated during nuclear accidents, spent fuel disposal, isotope source production, and other processes, in which there are usually a large number of non-radioactive ions such as K + , Na + , Ca 2+ , and Mg 2+ , as well as fission products such as Sr 2+ and lanthanide ions 2,7,8 .The complex environment and composition pose a great challenge to the selective separation of Cs + from various types of radioactive liquid waste.Ion exchange is considered to be an ideal method 9,10 .However, the anionic frameworks of traditional cation exchangers (e.g., ion-exchange resins, zeolites, clays, titanosilicates, and metal-organic frameworks) have strong Coulombic interactions with high-valency metal ions, and thus their Cs + capture properties are readily attenuated 7,[9][10][11][12][13] .In addition, K + (212 pm) and Na + (228 pm) ions with similar hydration radii to Cs + (219 pm) also significantly affect the Cs + capture 7,[12][13][14] .Metal sulfides are a new class of inorganic ion exchange materials developed in recent years 9,[15][16][17][18][19][20][21] .The strong affinity of Lewis soft base S 2− sites for Lewis soft acid Cs + ions and the flexible sulfide framework make them exhibit excellent removal ability for Cs + ions 9 .Recently, we have achieved the selective capture of Cs + in HNO 3 solutions containing excess interfering ions by a highly stable layered metal sulfide (InSnS-1) and confirmed that the selectivity originated from the H + inhibition mechanism and the Cs + •••S 2− strong interaction 19 .Under neutral conditions, a very small number of three-dimensional microporous metal sulfide ion exchange materials with suitable pore sizes show good selectivity for Cs + capture, but the pore size limitation also makes these materials inefficient for Cs + removal, which is manifested by limited adsorption capacity and slow adsorption rate 9,[22][23][24][25] .Although the adjustable interlayer spacing and readily exchangeable interlayer ions of layered sulfides allow them to capture Cs + efficiently, their Cs + capturing performance is greatly weakened by competing ions 9,26 .Therefore, it is still eager to develop the effective construction strategy for cesium scavengers to achieve efficient and highly selective capture of Cs + ions.
Molecular/ion imprinting is an emerging technology that has been widely studied and applied in the field of water treatment [27][28][29] .Imprinted adsorbents synthesized using customized templates (functional groups or functional monomers) have specific recognitionadsorption capabilities, which have been used for the removal of heavy metal ions and radioactive ions 28,30,31 .However, ion-imprinted polymers for selective Cs + capture are uncommon due to the limitation of functional monomer species 30,31 .Herein, we propose a strategy to use ion-imprinting technology for the preparation of inorganic materials.The imprinting effect of functional monomers on Cs + was simulated by taking advantage of the relatively robust framework structure of inorganic materials and the spatially confined effect of affinity sites on Cs + .The specific synthesis strategy is as follows.Firstly, nonradioactive Cs + ions are used to participate in material synthesis to construct frameworks with strong coordination ability for target nuclides ions (Cs + ).Then, the non-radioactive Cs + ions are removed from the material (e.g., activation by high concentration of K + ions), leaving sites with a strong affinity for the target nuclides ions (Cs + ) as well as a suitable space.This will allow the anionic framework of material to specifically recognize the target nuclides ions (Cs + ).In this work, the ion imprinting technique is successfully promoted to the preparation of inorganic adsorbents.The current strategy will combine the high selectivity advantage of imprinted adsorbents with the excellent irradiation resistance, environmental compatibility, and adsorption efficiency of inorganic adsorbents.Thus, the prepared "inorganic ion-imprinted adsorbents" will be more advantageous to radioactive waste treatment which generally faces the harsh environment.Based on this strategy, the selectivity of Cs + ion-imprinted metal sulfide scavenger for Cs + will further be enhanced due to the affinity of soft basic S 2− sites for Cs + .
Guided by the aforementioned strategy, we have successfully constructed a layered gallium thiostannate Cs 2.33 Ga 2.33 Sn 1.67 S 8 •H 2 O (FJSM-CGTS) that exhibits the imprinting effect on Cs + .Its K + activation product, Cs 0.51 K 1.82 Ga 2.33 Sn 1.67 S 8 •H 2 O (FJMS-KCGTS), exhibits excellent selectivity for Cs + removal.In Cs + solutions with excess competing ions (K + , Ca 2+ , Na + , Mg 2+ , Sr 2+ , and Eu 3+ ) or in environmental water samples, it can effectively remove low-concentration Cs + ions.It is recyclable and can be used as a stationary phase in ion exchange columns for fast and easy treatment of Cs + -containing solutions to achieve waste volume minimization.Attractively, FJSM-KCGTS demonstrates excellent treatment capabilities for actual 137 Cs-liquidwaste generated during industrial production.Moreover, the "ion imprinting" process was visually revealed by the single-crystal structure analyses.The selective adsorption mechanism and structurefunction relationship were clarified by structural comparative analysis and density functional theory (DFT) theoretical calculations from perspectives of structure and energy.The validity of the synthetic strategy for constructing "inorganic ion-imprinted adsorbents" was confirmed.It is unprecedented to use ion imprinting method for the highly selective capture of Cs + by inorganic materials.This work provides inspiration for the development of inorganic ion-imprinted scavengers with high selectivity for target radionuclides removal.

Synthesis and characterization
The light-pink plate-like crystals of FJSM-CGTS (Cs  1-5) and energy dispersive spectroscopy (EDS, Supplementary Fig. 1), thermogravimetric analysis (Supplementary Fig. 2) and inductively coupled plasma-optical emission spectroscopy (ICP-OES) test.Powder X-ray diffraction (PXRD) patterns are in agreement with three corresponding simulated PXRD pattern calculated from single-crystal X-ray data (Supplementary Fig. 3).Single-crystal Xray diffraction, EDS, elemental distribution maps and X-ray photoelectron spectroscopy (XPS, Supplementary Method 2.2) tests identify successful exchange between K + and Cs + , confirming the "ion imprinting" process (Supplementary Figs.3-5).Scanning electron microscope (SEM) images show that the ion exchange process of K + and Cs + had no significant effect on the morphology of materials (Supplementary Fig. 6).
FJSM-CGTS crystallizes in the Pmc2 1 space group.T2-[Ga 2.33 Sn 1.67 S 10 ] 6.33− clusters constructed from corner-sharing [(Sn/Ga) S 4 ] tetrahedra act as the secondary building blocks for the anionic layers of [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− in FJSM-CGTS (Fig. 1a).Each T2 cluster building block shares its four corners (μ 2 -S 2− ) with four neighboring T2 clusters, forming a wavy [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− layer (Fig. 1a).Cs + are distributed in an unorganized manner in the interlayer spaces (Fig. 1a).The close proximity between Cs2 and Cs2B leads to the inability of both positions to be occupied by Cs + at the same time, and similarly for Cs3 and Cs3B.By single-crystal structure analysis, both FJSM-KCGTS and FJSM-KCGTS-Cs maintain the layer structure of the parent (Supplementary Fig. 7).The schematic diagram of the "ion imprinting" process is shown in Fig. 1b.In FJSM-KCGTS, Cs + in the original Cs1 and Cs3/Cs3B positions were completely replaced by K + and Cs + in the Cs2/ Cs2B positions were partially replaced by K + .In FJSM-KCGTS-Cs, K + in the original Cs1 and Cs3/Cs3B positions were completely replaced by Cs and K + in the Cs2/Cs2B positions were partially replaced by Cs + .This may be due to the fact that Cs1 and Cs3/Cs3B are located in the interlayer spaces, and they are coordinated with seven or eight sulfurs from the different layers, respectively, whereas Cs2/Cs2B situate within the layer and are coordinated by eight sulfurs from the same layer (Fig. 1c and Supplementary Fig. 8).Therefore, Cs2/Cs2B are more difficult for ion exchange compared with Cs1 and Cs3/Cs3B resulting in the partial replacement of K + in Cs2/Cs2B positions.ORTEP-style illustrations of FJSM-CGTS, FJSM-KCGTS and FJSM-KCGTS-Cs are shown in Supplementary Fig. 9.

Efficient extraction of Cs +
FSJM-KCGTS obtained by K + activation of FJSM-CGTS (Supplementary Method 2.1 and Supplementary Fig. 10) was used for Cs + capture performance studies.The Cs + adsorption of FJSM-KCGTS can reach equilibrium within 5 min with the removal rate (R, Eq. (S1)) exceeding 99% (Fig. 2a), and the kinetic data are highly fitted with the pseudofirst-order kinetic model (Supplementary Fig. 11 and Supplementary Table 6).The Cs + concentration is dramatically reduced to a few tens of micrograms per liter, a reduction in concentration of two orders of magnitude.The Cs + adsorption isotherm data of FJSM-KCGTS at room temperature (RT) exhibits well-fitting to the Langmuir isotherm model with R 2 of 0.99 and the maximum exchange capacity (q m ) of 246.65 mg g −1 (Fig. 2b and Supplementary Table 7).The theoretical exchange capacity of FJSM-KCGTS for Cs + was 287.52 mg g −1 , calculated from the chemical formulae of FJSM-KCGTS and FJSM-KCGTS-Cs.The experimental values were slightly lower than the theoretical value which may be attributed to the fact that the exchanged K + would compete with Cs + .q m Cs of FJSM-KCGTS is higher than the reported Cs + ion-imprinted adsorbents, including Cs(I)-IIP2 (54.54 mg g −1 ) 32 , cesium ion-imprinted polymer based on dibenzo-24-crown-8 ether nanoparticles (50 mg g −1 ) 33 , and Cs(I) ion-imprinted polymer based on sodium trititanate whisker and chitosan (32.88 mg g −1 ) 34 .It is also more than many common Cs + adsorbents including zeolites (e.g., Turkish samples: 89.18 mg g −1 ) 35 , carbon-based (e.g., GO: 76.9 mg g −1 ) materials 36 , metal sulfides (e.g., KMS-1: 226 mg g −1 ) 37 , and the commercially available AMP-PAN (81 mg g −1 ) marketed by UOP as IONSIV IE-91 38 .

Selective capture of Cs +
The effect of competing ions (Na + , K + , Ca 2+ , Mg 2+ , Sr 2+ , and Eu 3+ ) on the selective capture behavior of Cs + ions by FJSM-KCGTS was systematically examined.K d Cs of FJSM-KCGTS can be maintained above 10 4 mL g −1 with R Cs > 91% when Na/Cs molar ratios are in the range of 27.1-1246.Even when Na/Cs molar ratio reaches 1.13 × 10 4 , K d Cs is still above 10 3 mL g −1 , with R Cs of 58.80% (Fig. 3a).Since the material contains K + , the excess K + in solution is bound to greatly affect the Cs + exchange compared to Na + ions (Supplementary Fig. 16).Even so, when K/Cs molar ratio is 408, K d Cs can attain 1.71 × 10 3 mL g −1 with R Cs of 63.11%.When Cs + coexists with the high-valency competing ion M n+ (M n+ = Ca 2+ , Mg 2+ , Sr 2+ , and Eu 3+ ), highly selective capture of Cs + by FJSM-KCGTS can also be observed (Fig. 3b-e and Supplementary Fig. 17).Under the low molar ratio of M/Cs, R Cs are more than 97.7% and K d Cs are higher than 10 4 mL g −1 .At this time, R M can also reach more than 68%.When the M/Cs molar ratio is increased by two orders of magnitude, R Cs decrease slightly, but still reach more than 73% with K d > 10 3 mL g −1 .The decrease of R Cs is relatively big in the coexisting Eu/Cs solution, from 98.90% to 73.55%, and the smallest decrease in R Cs is observed in the coexisting Ca/Cs solution, from 97.79% to 90.51%.By contrast, R M decreases dramatically, that is, R Ca , R Mg , R Sr , and R Eu decreased to 1.39%, 3.12%, 11.86%, and 17.39%, respectively.The above results show that FJSM-KCGTS had removal ability for both Cs + and M n+ under the low concentrations of both Cs + and M n+ .However, when the M n+ concentration is substantially increased, the adsorption performance of FJSM-KCGTS for Cs + is maintained at a high level, while the adsorption performance for M n+ is significantly reduced.That is to say, FJSM-KCGTS can still selectively capture low concentrations of Cs + ions in the presence of a large number of competing ions.We believe that the adsorption performance of FJSM-KCGTS for both Cs + and M n+ ions in low concentration solutions may originate from the redundancy of ion exchange active sites.Therefore, taking the coexisting Cs/Sr system as a representative, we further investigated the adsorption behaviors of FJSM-KCGTS under coexisting Cs/Sr with both of equimolar concentrations or equipotent charge concentrations.The same results are found under both conditions (Fig. 3f and Supplementary Fig. 18).Under low Cs + and Sr 2+ ion concentrations,  FJSM-KCGTS shows good removal performance for both Cs + and Sr 2+ ions, with K d Cs > 10 5 mL g −1 , K d Sr > 10 6 mL g −1 , R Cs > 99%, and R Sr > 99.9%.With the increase of both concentrations, the capture performance of FJSM-KCGTS for Sr 2+ decreases significantly, while the capture performance for Cs + is maintained.Specifically, in coexisting Cs/Sr solutions with equimolar concentrations or equipotent charge concentrations, R Cs can still reach 82.65% and 75.74% whereas R Sr decreases to 22.70% and 16.20%, respectively.This is attributed to the fact that under low concentrations of Cs/Sr ions, FJSM-KCGTS has an excess of ion exchange active sites, thus exhibiting removal of both Cs + and Sr 2+ .By contrast, the limited adsorption sites of FJSM-KCGTS can not accommodate all Cs + and Sr 2+ ions under high concentration of Cs + /Sr 2+ ions.Note that the removal performance of FJSM-KCGTS for Cs + still remain at a high level while the removal performance for Sr 2+ decreases significantly, indicating that FJSM-KCGTS has the ability to preferentially selectively capture Cs + .This excellent selectivity enable FJSM-KCGTS to achieve effective removal of Cs + from lake, river and seawater samples with added Cs + .Especially in complex seawater samples, it is rare that q m Cs can still reach 206.44 mg g −1 , proving that FJSM-KCGTS has the ultra-high selectivity for Cs + removal in highly saline environments (Supplementary Method 2.4, Supplementary Fig. 19 and Supplementary Table 8).
Therefore, the selective Cs + capture ability of FJSM-KCGTS is little weakened by the increased concentration of competing ions.It is noteworthy that this phenomenon is quite different from the reported results.The Cs + adsorption properties of most Cs + scavengers such as MOFs, clay minerals, and even some metal sulfide materials are significantly weakened by competing ions, especially high-valency ions 13,37,[39][40][41] .Some metal sulfide ion-exchange materials containing protonated organic amines can also capture Cs + after K + activation, but their capturing performance is also very susceptible to competing ions 40,42,43 .A very small number of three-dimensional materials with suitable pore size have good selectivity for Cs + capture 9,[22][23][24][25] .However, we found that the presence of competing Sr 2+ and Eu 3+ ions is also detrimental to their capture efficiency for Cs + (Supplementary Method 2.5 and Supplementary Figs.20 and 21).The selective Cs + capture performance of FJSM-KCGTS synthesized under the guidance of our strategy is at the forefront of reported materials, with high adsorption capacity, short adsorption equilibrium time and high selectivity.It suggests that the current "ion-imprinting effect" plays a key role in the Cs + capture process of FJSM-KCGTS.The design and synthesis strategy of the current material should be effective in significantly enhancing the selectivity for Cs + removal in neutral highsalinity solutions.

Column experiments
FJSM-KCGTS was packed into the ion exchange column as stationary phase to realize the adsorption and elution process of Cs + conveniently and efficiently (Supplementary Fig. 22).The breakthrough curve of Cs + ion adsorption conforms to the Thomas model (R 2 > 0.99) with q m Cs of 288.94 mg g −1 , and a treatment volume of about 4500 bed volumes when the breakthrough point (C t /C 0 = 0.05) is reached (Fig. 4a and Supplementary Table 9).In other words, about 540 mL of Cs + solution (C 0 = 31.995mg L −1 ) can be effectively treated to produce only one bed volume (0.12 mL) of solid waste, resulting in a three-order-ofmagnitude reduction in waste volume.Note that unlike isothermal adsorption experiments, the exchanged K + ions are eluted out of the adsorption column in the column experiments and do not affect the adsorption of Cs + .Therefore, the dynamic adsorption capacity is comparable to the theoretical value (287.52 mg g −1 ).Such dynamic capture performance of Cs + ions exceeds most reported Cs + ion exchangers such as InSnS-1, MCC-g-AMP, M/SZMs, and PEI/ZnFC 19,[44][45][46] .After reaching the saturation adsorption, the adsorbed Cs + ions can be leached off with 1 mol L −1 NH 4 Cl solution (Fig. 4b).It is noteworthy that the Cs + ions concentration in the first four eluent samples (totaling 12 mL) reaches more than 10 3 mg L −1 .The first 16 eluent samples (totaling 12 mL) can elute 32.10 mg of Cs + ions with elution rate (R E ) of 95.65% (Supplementary Method 2.5).Therefore, the ion exchange column filled with FJSM-KCGTS can quickly and effectively enrich and concentrate Cs + ions.FJSM-KCGTS has the potential for engineering treatment of radiocesium-containing waste liquids to realize waste liquid volume reduction.Actual 137 Cs-liquid-waste treatment FJSM-KCGTS was used for the treatment of neutral and acidic (pH = 2.6) 137 Cs-liquid-waste generated from the production of radioactive sources at CNNC HTA Co., ltd.Both solutions contained 60 Co 2+ and Na + ions and so on in addition to 137 Cs + .The experimental results show that only 5 mg of FJSM-KCGTS can remove 94.09% and 89.93% of 137 Cs from 5 mL neutral and acidic 137 Cs-liquid-waste, respectively (Fig. 4c, d).When 40 mg of FJSM-KCGTS is used (solid-liquid ratio m/V = 8 mg mL −1 ), R Cs-137 reaches 99.45% and 98.42%, respectively, and the 137 Cs activity concentrations of both wastewaters are reduced by two orders of magnitude.Therefore, a small amount of FJSM-KCGTS can significantly reduce the radioactivity of wastewater, which contributes to the effective reduction of the volume of radioactive waste.FJSM-KCGTS shows excellent 137 Cs removal performance under actual working conditions, which highlights a 137 Cs scavenger with practical application potential.

Density functional theory calculations
In order to further elucidate the mechanism of the highly selective capture of Cs + by FJSM-KCGTS, DFT calculations of the interaction of the [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− layer with M n+ (M n+ = Cs + , K + , Na + , Sr 2+ , and Eu 3+ ) ions were performed.DFT results show that the binding energies of Cs + , K + , Na + , Sr 2+ , and Eu 3+ ions to anionic layers are −5.10,−4.82, −4.51, −7.07, and −7.32 eV, respectively (Fig. 5).The binding energies of Na + and K + to anionic layers are lower than that of Cs + , suggesting stronger interactions between anionic layers and Cs + ions.The binding energies of Sr 2+ and Eu 3+ ions to anionic layers are higher than that of K + ions, but each Sr 2+ and Eu 3+ ion need to displace two and three K + ions, respectively.Therefore, this process requires a higher energy than the replacement of K + ions with Cs + ions.DFT results confirm that FJSM-KCGTS possesses the stronger selectivity for Cs + than Na + , K + , Sr 2+ , and Eu 3+ from view of energy, which are consistent with the phenomena observed in systematic selectivity experiments.

Capture mechanism and structure-function relationship
Combined with the above experiments and characterization data, the selective capture ability of FJSM-KCGTS for Cs + is believed to originate from the synergistic action of the ion exchange and the imprinting effect.Single-crystal structure analyses clearly and visually demonstrate the whole process of "ion-imprinted" Cs + capture by FJSM-CGTS as well as the coordination pattern of Cs•••S.FJSM-CGTS shows more outstanding Cs + selectivity than reported Cs + ion exchangers such as KMS-1 37 , KMS-2 16 , KTS-3 17 , and FJSM-SnS 18 .Because the anionic layers of these reported Cs + ions scavengers are plate-like (Supplementary Fig. 23a), the entry of Cs + ions into the interlayer space causes a significant change in layer spacing (Supplementary Table 10).For example, KMS-1 and FJSM-SnS captured Cs + with an increase or decrease in layer spacing of 0.49 Å and 0.549 Å, respectively.The flexible and adjustable interlayer spacing characteristic of these ion exchangers makes them easily accommodate foreign ions, which may lead to their relatively poor selective capture of Cs + .However, the [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− anionic layers of FJSM-KCGTS are wavy-like (Supplementary Fig. 23b).During K + activation and Cs + adsorption, the layer spacing variation of FJSM-CGTS was less than 0.25 Å.This may be due to the fact that the wavy layers stacking pattern produces stronger interlayer interactions than planar layers stacking pattern, favoring the reduction of layer spacing variations.The relatively robust wavy-layer structure of FJSM-CGTS provides a suitable spatial and coordination environment for Cs + , which can be regarded as "Cs + recognition sites".These sites are more suitable for accommodating and "anchoring" Cs + ions, even after the sites are occupied by K + ions.Therefore, we suggest that the wavy layered structure and the strong interaction of soft basic S 2− sites with Cs + provide a spatially confined effect on Cs + , contributing to the excellent selectivity of FJSM-KCGTS for Cs + capture.DFT results also confirm this point from an energetic viewpoint.
The unparalleled Cs + capture performance of FJSM-CGTS (FJSM-KCGTS) proves the effectiveness of the "inorganic ion-imprinted adsorbent" synthesis strategy.The advantages of ion exchangers and imprinted adsorbents were combined to make "inorganic ionimprinted adsorbents" with high adsorption efficiency and outstanding selectivity.By utilizing the "imprinting effect" generated by the spatially confined effect, highly selective recognition and capture of target ions can be achieved.Notably, the "imprinting effect" of the current material originating from a specific structure of inorganic material is expected to reduce the constraints imposed by the type of functional groups or functional monomers on the development of imprinted polymers because of the variety, tunability, and designability of the frameworks of inorganic materials.

Discussion
We propose a strategy to construct the "inorganic ion-imprinted adsorbent" that utilizes the spatially confined effect from the robust framework of inorganic materials to achieve "imprinted adsorption" of target ions.Under the synergistic action of ion exchange and "imprinting effect", the inorganic layered metal sulfide FJSM-CGTS (FJSM-KCGTS) prepared based on this strategy overcomes the defect that the performance of traditional Cs + ion exchangers is greatly weakened by competing ions, especially high-valency ions, and it can selectively recognize and capture Cs + .It can be used as a stationary phase for ion-exchange columns to realize the volume reduction and concentration of Cs + -containing solutions quickly and conveniently.Importantly, FJSM-KCGTS demonstrates excellent treatment capability for actual 137 Cs-liquid-waste generated during industrial production.Single-crystal structure analysis "visualizes" the whole process of "ion-imprinted" adsorption for Cs + , and theoretical calculations reveal that the strong binding force of the anionic sulfide framework to Cs + is the source of the high selectivity of FJSM-KCGTS.The excellent Cs + capture performance of FJSM-KCGTS proves the effectiveness of our synthesis strategy.The high selectivity of the imprinted adsorbent and the stability, high adsorption efficiency and good environmental compatibility of the inorganic adsorbent material can be combined through this strategy to prepare a new "inorganic ion-imprinted adsorbent" that is more suitable for the treatment of radioactive waste liquids.This study pioneers the preparation of inorganic materials with ion-imprinting functionality.The clear illumination on the selective adsorption mechanism and structure-function relationship provides the direction for developing efficient inorganic adsorbents with the ability of specifically recognition-separation for key radionuclides.

Synthesis of FJSM-KCGTS
Five hundred mg of FJSM-CGTS crystals were mixed with 500 mL solution of 2 mol L −1 KCl and the mixture was shaken for 24 h at RT. Then the crystals were washed with deionized water and ethanol, and dried naturally to afford the FJSM-KCGTS.

Synthesis of FJSM-KCGTS-Cs
Five hundred mg of FJSM-KCGTS crystals were mixed with 500 mL solution of 5000 mg L −1 Cs + ions and shaken for 12 h at RT. Then the crystals were washed with deionized water and ethanol, and dried naturally to afford the FJSM-KCGTS-Cs.

Batch ion exchange experiments
In order to reduce the generation of radioactive waste during the experiments, non-radioactive Cs + ions were used to simulate 137 Cs + ions for both batch ion exchange experiments and column experiments.A typical ion exchange experiment with FJSM-KCGTS was performed in a 20 mL polyethylene bottle containing an aqueous solution of cesium chloride (V/m = 1000 mL g −1 ) and FJSM-KCGTS crystals.The polyethylene bottles containing the solid-liquid mixture were shaken in an oscillator at RT for 4 h and then left to stand for a few minutes.The supernatant was filtered through a filter with a 0.22 μm membrane and diluted to the appropriate concentration range for ICP testing.The removal rate (R) and distribution coefficient (K d ) could be calculated by Eqs. ( 1) and (2) (Supplementary Notes 1), respectively.The solid samples were washed several times with deionized water and anhydrous ethanol before drying.
In FJSM-CGTS activation kinetic experiments, 50 mg of FJSM-CGTS crystals were added to 50 mL of 2 mol L −1 KCl solution under magnetic stirring at RT.The suspension was sampled at different time intervals and then filtered to test the concentration of Cs + in the solution.In the Cs + adsorption kinetic experiments by FJSM-KCGTS, 50 mg of FJSM-KCGTS crystals were added to 50 mL of 8.53 mg L −1 CsCl solution under magnetic stirring at RT.The suspensions were sampled at different time intervals and then the solution samples were obtained by filtration to test the Cs + concentrations.The kinetic data of Cs + capture by FJSM-KCGTS were fitted with the pseudo-first-order kinetic model (Supplementary Notes 1, Eq. ( 3)) than the pseudo-second-order kinetic model (Supplementary Notes 1, Eq. ( 4)).
In the adsorption-desorption cycling experiment, 250 mg of FJSM-KCGTS-Cs was mixed with 250 mL of 1 mol L −1 NH 4 Cl solution and shaken for 24 h to fully elute Cs + adsorbed by the material.Using the sample obtained at this time as the initial material for the cycling experiments ensures the consistency of the material used in each round of cycling.Each cycle contains two phases of adsorption and desorption.The solution used in the adsorption process was 79.45 mg L −1 CsCl solution with a contact time of 4 h.The solution used in the desorption process was 1 mol L −1 NH 4 Cl solution with a contact time of 12 h.After the completion of each adsorption/desorption, the supernatant was used to determine the Cs + concentration after filtration and dilution.The desorption rate could be calculated by Eqs. ( 9)-(11) (Supplementary Notes 1).The solid samples were washed and dried and then partially used for PXRD test to confirm the framework stability of the compounds and partially used for the next round of adsorption/desorption experiments.The solid samples used in each adsorption/desorption experiment were weighed and added to the corresponding amount of solution to ensure a solid-liquid ratio of 1000 mg L −1 .
Actual 137 Cs-liquid-waste treatment test The thermal test was conducted using 137 Cs-liquid-waste generated by Atomic High Tech of CNNC in industrial production.The initial activity concentrations of the generated neutral or acidic (pH = 2.6) 137 Csliquid-wastes were 8.78 × 10 4 Bq mL −1 and 1.53 × 10 4 Bq mL −1 , respectively, and the conductivities were 9.72 mS cm −1 and 12.06 mS cm −1 , respectively.Five mg, 10 mg, and 40 mg of FJSM-KCGTS were added to 5 mL of neutral or acidic 137 Cs waste solution, respectively.After shaking for 6 h, the supernatant was filtered and the activity of 137 Cs was measured by a γ-hole counter.

Column experiments
In total, 0.095 g of FJSM-KCGTS crystal sample was loaded into a polyethylene column with an inner diameter of 4.50 mm.The loading height was approximately 7.56 mm and the bed volume was 0.12 mL.A sieve plate with a pore size of 10 μm was placed at the bottom of the column to avoid loss of solid sample.A solution of 31.995mg L −1 Cs + was passed through the ion exchange column at a flow rate of 0.6 mL min −1 (5 BV min −1 ).The adsorption data were fitted with the Thomas model (Supplementary Notes 1, Eq. ( 12)).After adsorption was completed, the adsorbed Cs + was eluted using 1 mol L −1 NH 4 Cl solution as a drench solution.Samples of the effluent solution were collected in polyethylene tubes within each 5-min period and the measured concentration was approximated to the concentration at the intermediate moment.The Cs + ions concentration of the eluate collected from each tube was determined, and the total amount of Cs + eluted down could be calculated.The desorption rate could be calculated by Eq. ( 13) (Supplementary Notes 1).Solution flow rate and sample collection are controlled by a peristaltic pump and automatic collector.

Density functional theory calculations
All calculations were performed using the Vienna Ab-initio Simulation Package (VASP, version number 6.2.1) with spin-polarized density functional theory (DFT) methods [47][48][49] .The generalized gradient approximation (GGA) with the Perdew-Burke-Ernzerhof (PBE) functional are used to describe the exchange and correlation energies 50,51 .The projector augmented-wave (PAW) method was used to describe the electron-ion interactions.Based on careful convergence tests, the plane wave energy cutoff was set to 400 eV.The convergence criterion of electronic structure was set to 10 −4 eV.The atomic relaxation was continued until the forces acting on atoms were smaller than 0.05 eV Å −1 .The Brillouin zone was sampled in a k-point mesh with the separation of 0.04 Å −1 .The Gaussian smearing of 0.05 eV was applied in order to speed up electronic convergence.In order to avoid the unwanted interaction between the slab and its period images, a vacuum height of 15 Å along the vertical direction was chosen.The adsorption binding energies (E ads ) used in this paper were calculated based on Eq. ( 14) (Supplementary Notes 1).

Fig. 1 |
Fig. 1 | Schematic diagram of the structure of FJSM-CGTS and the "ion imprinting" process.a A T2-[Ga 2.33 Sn 1.67 S 10 ] 6.33− cluster, an anionic layer of [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− and view of layers stacking in FJSM-CGTS along a axis.Cs2B, Cs3B, O, and H are ignored for clarity.b Schematic diagram of the "ion imprinting" process for the selective capture of Cs + by the current layered metal sulfide and the

Fig. 3 |Fig. 2 |
Fig. 3 | Selective removal of Cs + by FJSM-KCGTS in the presence of competing ions.The selective capture of Cs + by FJSM-KCGTS in the presence of competing ions.K d Cs and R Cs values of FJSM-KCGTS in neutral solutions with different (a) Na/Cs molar ratios.R of Cs + and M n+ (M n+ = Ca 2+ , Mg 2+ , Sr 2+ , and Eu 3+ ) ions removed by FJSM-KCGTS in neutral solutions with different (b) Ca/Cs, (c) Mg/Cs,

Fig. 4 |
Fig. 4 | Exploration of the practical application potential of FJSM-KCGTS for Cs + capture.a The Cs + capture breakthrough curve and (b) elution curve of FJSM-KCGTS packed column.Treatment capacity of FJSM-KCGTS for (c) neutral and (d) acidic (pH = 2.6) 137 Cs liquid-waste plotted as the activity concentration and the R of 137 Cs + vs. the mass of adsorbent (mg), respectively.Source data are provided as a Source Data file.

Fig. 5 |
Fig. 5 | Results of density functional theory calculations.The calculation on binding energies of the [Ga 2.33 Sn 1.67 S 8 ] n 2.33n− layer (abbreviated as "GTS layer" in the figures) to (a) K + , (b) Na + , (c) Cs + , (d) Sr 2+ , and (e) Eu 3+ ions.The atomic coordinates of the optimized computational models are provided in Supplementary Data 1.